C.V. Compressor. Assume adiabatic and neglect kinetic energies
Energy Eq. w = h1 - h2
Entropy Eq s2 = s1 + sgen
We have two different cases, the ideal and the actual compressor.
States: 1: h1 = 1188.36 Btu/lbm, s1 = 1.601 Btu/lbm R
2ac: h2,AC = 1598.6 Btu/lbm, s2,AC = 1.6398 Btu/lbm R
2s: F.7.2 (P, s = s1) h2,s = 1535.1 Btu/lbm